TY - JOUR
T1 - Integrated development of fermentation and downstream processing for L-isoleucine production with Corynebacterium glutamicum
AU - Weuster-Botz, D.
AU - Karutz, M.
AU - Joksch, B.
AU - Schärtges, D.
AU - Wandrey, C.
PY - 1996
Y1 - 1996
N2 - Applying a genetic algorithm for the optimization of trace element composition in the medium for L-isoleucine production from glucose and DL-α-hydroxybutyric acid with Corynebacterium glutamicum resulted in a reduction of the byproduct L-valine. High L-isoleucine broth concentrations of 20 g/l within 72 h at an L-isoleucine/DL-α-hydroxy butyric acid yield of 70% (w/w) and an L-isoleucine/L-valine ratio of 100 were achieved, if closed-loop control of glucose and of DL-α-hydroxybutyric acid was applied. For the isolation of L-isoleucine from fermentation broth a specific downstream processing was developed and optimized up to semitechnical scale (ultrafiltration, reverse osmosis, first crystallization, active-carbon adsorption, electrodialysis, second crystallization). The economic model of this downstream processing, which was identified by coupling the mass balance and energy balance with the semi-empirical models of the unit operations, was used to quantify the isolation costs as a function of L-isoleucine concentration and L-isoleucine/L-valine ratio in the fermentation broth. A cost reduction for downstream processing from DM 55 to DM 25 (kg L-isoleucine)-1 and an improvement of the L-isoleucine yield in downstream processing from 48% to 80% was achieved using this economic model as the objective function to be minimized by the fermentation process (scenario: production of 70 tonnes L-isoleucine/year).
AB - Applying a genetic algorithm for the optimization of trace element composition in the medium for L-isoleucine production from glucose and DL-α-hydroxybutyric acid with Corynebacterium glutamicum resulted in a reduction of the byproduct L-valine. High L-isoleucine broth concentrations of 20 g/l within 72 h at an L-isoleucine/DL-α-hydroxy butyric acid yield of 70% (w/w) and an L-isoleucine/L-valine ratio of 100 were achieved, if closed-loop control of glucose and of DL-α-hydroxybutyric acid was applied. For the isolation of L-isoleucine from fermentation broth a specific downstream processing was developed and optimized up to semitechnical scale (ultrafiltration, reverse osmosis, first crystallization, active-carbon adsorption, electrodialysis, second crystallization). The economic model of this downstream processing, which was identified by coupling the mass balance and energy balance with the semi-empirical models of the unit operations, was used to quantify the isolation costs as a function of L-isoleucine concentration and L-isoleucine/L-valine ratio in the fermentation broth. A cost reduction for downstream processing from DM 55 to DM 25 (kg L-isoleucine)-1 and an improvement of the L-isoleucine yield in downstream processing from 48% to 80% was achieved using this economic model as the objective function to be minimized by the fermentation process (scenario: production of 70 tonnes L-isoleucine/year).
UR - http://www.scopus.com/inward/record.url?scp=0029953355&partnerID=8YFLogxK
U2 - 10.1007/s002530050807
DO - 10.1007/s002530050807
M3 - Article
AN - SCOPUS:0029953355
SN - 0175-7598
VL - 46
SP - 209
EP - 219
JO - Applied Microbiology and Biotechnology
JF - Applied Microbiology and Biotechnology
IS - 3
ER -